TRANSESTERIFICATION OF METHANOL WITH ETHYL ACETATE AND ETHANOL WITH METHYL FORMATE CATALYZED BY DBN

采用三步合成了１，５二氮杂环双环［４，３，０］壬烯５（ＤＢＮ）并考察了其在酯交换反应中的催化活性。结果表明，在没有环氧丙烷（ＰＯ）助剂存在时，ＤＢＮ的催化活性很低；但在有ＰＯ助催化剂存在时，ＤＢＮ对酯交换反应的催化活性极高，其催化活性随ＤＢＮ和ＰＯ浓度的增加而增大。考察了反应温度对ＤＢＮ催化剂的酯交换活性的影响，提出了酯交换反应的催化机理。     

脱氧核糖核酸变性和损伤的吸附伏安法研究

本文用汞电极（ＨＭＤＥ）二次导数阴极吸附伏安（ＳＤ－ＡｄＣＳＶ）和碳电极（ＧＣＥ、ＣＰＥ）导数循环伏安（ＦＤ－ＣＶ）法研究了核酸受热、紫外线、超声波和丝裂霉素Ｃ（ＭＭＣ）作用下的变性作用。在０．１ｍｏｌ／Ｌ（Ｋ２ＨＰＯ４＋ＫＨ２ＰＯ４）－０．１ｍｏｌ．Ｌ ＮａＣｌ（ｐＨ７．０）底液中，吸附的单股（ｓｓ－）和双螺旋（ｄｓ－）ＤＮＡ分别在ＨＭＤＥ上得到特征还原峰Ｐ３和Ｐ２，和在碳电极上得到氧化峰Ａ。物     

单茂钛催化剂的丙烯无规聚合反应及其动力学研究

比较了不同钛化合物／甲基铝氧烷（ＭＡＯ）催化体系的丙烯无规聚合，催化活性次序为ＣｐＴｉ（ＯＲ）３＞ＣｐＴｉ（ＯＰｈ）３＞ＣｐＴｉＣｌ３＞Ｃｐ２ＴｉＣｌ２＞Ｔｉ（ＯＢｕ）４＞ＴｉＣｌ４＞Ｔｉ（ＯＢｕ）２Ｃｌ２，所得聚丙烯用沸庚烷抽提８ｈ，溶解９５％以上，可溶部分经１３Ｃ ＮＭＲ、ＷＡＤＸ、ＦＴＩＲ等分析证明为无规聚丙烯（ａＰＰ），是没有结晶性的弹性体．ＧＰＣ测出其分子量Ｍｗ＝８．０～１０．０×１０４，Ｍｗ／Ｍｎ≈２．０．探索了催化体系ＣｐＴｉ（Ｏ ｎ Ｐｒ）３／ＭＡＯ中钛的浓度、［Ａｌ］／［Ｔｉ］摩尔比，丙烯聚合压力，聚合温度和时间对丙烯聚合反应的影响．研究了该催化体系丙烯聚合反应动力学规律，表观聚合反应速率对催化剂浓度和单体压力（浓度）都呈一级反应关系，表观聚合速率常数ＫＰ＝２９２×１０５ｍｏｌ／Ｌ·ｈ（４０℃）．活化能ΔＥ＝－７．８８×１０３Ｊ·ｍｏｌ－１，碰撞因子Ａ＝１．４１×１０－４ｍｏｌ／Ｌ·ｈ．     

丙醛均相催化加氢制丙醇的研究

系统地研究了在４．０ＭＰａ氢压下，反应温度、催化剂浓度、溶剂等对丙醛均相加氢制正丙醇反应的影响，得出最佳反应条件为：氢压４．０ＭＰａ、温度８０℃，ＲｕＣｌ３·３Ｈ２Ｏ为催化剂前体，用量９８ｍｇ（０．３５ｍｍｏｌ），ＰＰｈ３为３９３ｍｇ（１．５ｍｍｏｌ），Ｒｕ／Ｐ摩尔比为１／４，ＤＭＦ为溶剂．在此条件下，丙醛转化率和正丙醇选择性可分别达９９％和９５％以上．求出了不同反应温度下的反应速度常数．以ＲｕＣｌ３－ＰＰｈ３为催化剂体系，丙醛加氢的活化能为７７．６２ｋＪ／ｍｏｌ     

紫外分光光度-CPA矩阵法同时测定2-(2′-呋喃基)苯并咪唑和邻苯二胺

研究了２－（２′－呋喃基）苯并咪唑（ＦＢＤ）和邻苯二胺（ＯＰＡ）在无水乙醇溶液中的紫外吸收光谱，建立了多波长同时测定ＦＢＤ和ＯＰＡ的紫外光度ＣＰＡ矩阵法。ＦＢＤ和ＯＰＡ分别在０．１～１０ｍｇ／Ｌ和１．０～１００ｍｇ／Ｌ的浓度范围，ＦＢＤ和ＯＰＡ的回收率均大于９３％，相对标准偏差小于７．５％。     

Fe（Ⅲ）—TEA—5—Br—PADAP—H2O2体系中催化波的研究及其应用

在０．２ｍｏｌ·Ｌ＾－１ＮＨ４Ｃｌ－ＮＨ３·Ｈ２Ｏ底液中，（ｐＨ为９．２６），得到一个极为灵敏的Ｆｅ（Ⅲ）－ＴＥＡ－５－Ｂｒ－ＰＡＤＡＰ－Ｈ２Ｏ２配合吸附催化波，其峰电位为－０．７１Ｖ（ｖｓ．ＳＣＥ）。铁浓度在１．８×１０＾－１０￣５．４×１０＾－６ｍｏｌ·Ｌ＾－１范围内与二阶导数波高呈线性关系。对该极谱波的性质进行了研究，证明是一种配合吸附催化波，并成功地应用于各类水样，钒催化剂中微量或痕量铁的     

Fe（Ⅲ）－TEA－5－Br－PADAP－H_2O_2体系中催化波的研究及其应

在０．２ｍｏｌ·Ｌ￣（－１）ＮＨ＿４Ｃｌ－ＮＨ＿３·Ｈ＿２Ｏ底液中，（ｐＨ为９．２６），得到一个极为灵敏的Ｆｅ（Ⅲ）－ＴＥＡ－５－Ｂｒ－ＰＡＤＡＰ－Ｈ＿２Ｏ＿２配合吸附催化波，其峰电位为－０．７１Ｖ（ｖｓ．ＳＣＥ）。铁浓度在１．８×１０￣（－１０）～５．４×１０￣（－６）ｍｏｌ·Ｌ￣（－１）范围内与二阶导数波高呈线性关系。对该极谱波的性质进行了研究，证明是一种配合吸附催化波，并成功地应用于各类水样，钒催化剂中微量或痕量铁的测定。     

Ni—Mo—PTFE复合电极的制备及其对甲醇电氧化的催化性能

在０．２２ｍｏｌ／Ｌ硫酸镍，０．０６ｍｏｌ／Ｌ钼酸钠，０．３ｍｏｌ／Ｌ柠檬酸钠，３０ｇ／ＬＰＴＦＥ乳液，０．１ｇ／ＬＦＣ－４００表面活性剂的电解液（ｐＨ＝９）中，于温度４５℃，通以１０ｍＡ／ｃｍ２的电流，在纯Ｃｕ片上沉积出Ｎｉ－Ｍｏ－ＰＴＦＥ复合沉积层，ＸＲＤ、ＸＰＳ表征结果表明，该复合沉积层属立方晶系，其点阵型式为面心点阵Ｆ，晶胞参数ａ为０．３５７３ｎｍ，镍钼合金为固溶体结构，其（１１１）织构度ＴＣ（１１１）为６８％，表明该沉积层呈（１１１）择优取向．沉积层表面的氟以（ＣＦ２）ｎ的形式存在，ＳＥＭ观察结果表明沉积层含有ＰＴＦＥ时表面的粗糙度增大．镍－钼－ＰＴＦＥ复合电沉积过程经历吸附态物种氢氧化镍和钼的氧化物，它们继续捕获电子被还原为镍钼合金，ＰＴＦＥ粒子以包埋的形式沉积于镀层中．循环伏安结果表明该复合电极在ＮａＯＨ溶液中对甲醇的电氧化具有催化活性．     

固定化米曲霉催化拆分丙氨酸消旋体的反应特性

研究了溶液ｐＨ、搅拌强度，催化剂用量、底物浓度及产物浓度对固定化米曲霉催化拆分Ｎ－乙酰－ＤＬ－丙氨酸反应的影响。结果表明，低底物浓度（Ｓ〈０．２ｍｏｌ／Ｌ）时反应符合Ｍ－Ｍ方程，底物浓度Ｓ〉０．２ｍｏｌ／Ｌ时，有底物抑制现象，当产物浓度Ｐ〉１０ｍｍｏｌ／Ｌ时反应存在产物抑制现象。     

磷钼杂多酸-L-半胱氨酸自组装超分子膜电极对亚硝酸根电催化还原的研究

制备了磷钼杂多酸－Ｌ－半胱氨酸自组装超分子膜电极（Ｐ２Ｍｏ１８－Ｌ－Ｃｙｓ／Ａｕ）。采用水平衰减全反射（ＡＴＲ－ＦＴＩＲ）光谱表征了膜的组成。研究了该膜电极的电化学性质，发现它在１．０ ｍｏｌ／Ｌ　Ｈ２ＳＯ４溶液中，于０．０～０．７Ｖ（ｖｓ．ＳＣＥ）间ＣＶ扫描出现两对稳定、可逆的氧化还原峰，其中峰电位分别为Ｅｍ１＝０．３３４ Ｖ，Ｅｍ２＝０．１８８Ｖ，对应着Ｐ２Ｍｏ１８Ｏ_(６２)~(６－)的两步２电子－２质子反应；计时库仑法计算了薄膜内的电子传递系数Ｄ为５．０１ × １０~（－８）ｃｍ２·ｓ～（－１）。该膜电极对酸性溶液中的ＮＯ_２~－有明显的电催化还原作用，初步探讨了电催化机理。用差分脉冲伏安法（ＤＰＶ）测定其还原峰电流与ＮＯ_２~－的浓度在２．０ ×１０~（－６）～２．０ × １０~（－４）ｍｏｌ／Ｌ范围内呈良好的线性关系，相关系数为０．９９５３，检测限５．０×１０~（－７）ｍｏｌ／Ｌ。该电极用于模拟水样中ＮＯ_２~－的测定，结果满意。     

Kinetics of hydroformylation of 1-decene using carbon-supported ossified HRh(CO)(TPPTS)3 catalyst

The kinetics of hydroformylation of 1-decene has been investigated using a carbon-supported ossified HRh(CO)(TPPTS)₃/Ba catalyst in a temperature range of 343–363 K. The effect of concentration of 1-decene, catalyst loading, partial pressure of H₂ and CO, and stirring speed on the reaction rate has been investigated. A first-order dependence was observed for catalyst concentration and hydrogen partial pressure. The rate showed a typical case of substrate inhibition for high 1-decene concentration. The rate varied with a linear dependence on P_CO up to a CO partial pressure of 5–6 MPa in contrast to the general trends; for most of the rhodium-phosphine catalyzed hydroformylation reactions, severe inhibition of rate is observed with an increase in CO pressure. A rate equation has been proposed, which was found to be in good agreement with the observed rate data within the limit of experimental errors. The kinetic parameters and activation energy values have been reported.     

乙醇直接气相羰基化新催化剂

醇的羰基化合成是极有工业价值的过程 ,也是绿色化学中提倡的原子经济性反应 [1] .甲醇均相羰基化合成醋酸是 Monsanto公司成功开发应用的典范 [2 ] ,而乙醇羰基化合成丙酸或丙酸乙酯的研究尤其重要 .前文对一种性能优良的负载型 Ni系催化剂用于乙醇常压气相羰基化合成丙酸及其酯作了报道 [3,4] ,与均相羰基化相比 ,该反应具有条件温和 ,不使用贵金属铑 ,催化剂与产物不存在分离上的困难等优点 ,但反应体系仍需使用卤化物作促进剂 .由于碘乙烷的存在 ,反应系统设备腐蚀严重 (有 HI生成 ) ,产物分离精制复杂 .目前 ,醇的均相羰基化及多相羰…     

SYNTHESIS OF DBN AND ITS CATALYTIC PERFORMANCE FOR METHANOL CARBONYLATION TO METHYL FORMATE

1 , 5-diazabicyclo['1, 3, 0]non-5-ene(DBN) has been synthesized in our laboratory, and its catalytic activity and selectivity for methanol carbonylation to methyl formate (MF) have been studied. The experimental results have demonstrated that the synthetic processes of DBN used for the present work are reasonable and feasible. The total yield of three steps of DBN synthsis is approximate to 80%. The activity evaluation has shown that DBN can effectively catalyze the carbonylation reaction of methanol in the presence of propylene oxide (PO) promoter. PO-promoted DBN is a novel catalytic system superior to sodium methoxide.     

Direct Vapor Phase Carbonylation of Methanol over NiCl2/C Catalyst

IntroductionThe carbonylation of alcohols via homogenous catalysis is important in manufacturingacetic acid and higher carboxylic acids and their esters[1 ,2 ] . The main route to produce aceticacid is to make methanol carbonylated by means of the Monsanto and BP process in which ahomogeneous rhodium catalystis used.Although the homogeneous carbonylation ofmethanolis a highly selective process,itisaffected by the disadvantagesassociated with a highly corro-sive reaction medium due to the use …     

PVP-PdCl2-CuCl2/PPh3体系催化α-（6’-甲氧基-2’-萘基）乙醇羰化反应研究

首次用高分子负载型双金属催化剂PVP-PdCl2-CuCl2/PPh3体系催化α-（6’-甲氧基-2’-萘基）乙醇与一氧化碳及甲醇进行羰化反应制备萘普生甲酯, 分别对温度、压力、时间、 P/Pd比等影响因素进行了考察, 在反应条件为100 ℃、 16～20 h、 CO压力 4.0 MPa、 P/Pd=3时, 转化率可达97.4%, 异正比为14.4. 在同样条件下制备萘普生乙酯及萘普生异丙酯, 转化率及选择性均有明显下降. 另外, 该催化剂体系也可催化其它类型α-芳基乙醇的羰化反应.     

钛硅分子筛催化丙烯环氧化反应条件的研究

以用四丙基溴化铵（ＴＰＡＢｒ）为模板剂合成的钛硅分子筛ＴＳ－１为催化剂，Ｈ２Ｏ２为氧化剂，系统地研究了丙环氧化反应的规律，考察了反应温度、丙烯压力、催化剂用量、反应时间等反应参数的影响，找到了较佳的丙烯环氧化反应条件。研究发现：温度对反应结果有显著影响。随反应温度升高，Ｈ２Ｏ２转化率提高，但环氧丙烷（ＰＯ）选择性降低；丙烯压力对反应结果无明显影响，催化剂不经再生处理，多次重复使用产物分布保持不变，     

双金属催化环氧化物聚合动力学研究

研究了双金属氰化络合催化剂DMC催化环氧丙烷聚合的动力学 .用测定反应过程体系压力变化来决定聚合的起始速率 ,发现聚合反应速率正比于催化剂用量C ,单体浓度M的平方 .该实验规律可以从单体参与链引发的动力学特点解释 .考察了温度对聚合反应速率的影响并求得了表观活化能为 5 9 1kJ·mol- 1 ,该值与环氧聚合的卟啉铝、稀土络合物等催化体系接近 .     

A Novel Sul ded Mo/C Catalyst for Direct Vapor Phase Carbonylation of Methanol at Atmospheric Pressure

The direct carbonylation of methanol, without any halide in the feed as a promoter, is presented. A series of Mo catalysts supported on activated carbon, y-Al2O3 and SiO2 were prepared. The results show that the support greatly affects the Mo catalyst in the direct vapor-phase carbonylation of methanol, and activated carbon is the best supports of the investigated supports. In addition, the relationships between adsorptions of NH3 and CO and carbonylation of methanol were investigated. A novel sulfided Mo/C catalyst had high activity and selectivity for the vapor phase carbonylation of methanol to methyl acetate without the addition of a CH3I promoter to the feed. The reaction conditions were optimized at a reaction temperature of 573 K, a methanol concentration of 23 mol% and a carbon monoxide space velocity of 3,000 L/(kg-h). Under these optimal conditions a methanol conversion of 50%, carbonylation selectivity of 80 mol%, and space-time yield of 8.0 mol/(kg-h) were obtained. The active phase of this     

Kinetic studies on vapor phase carbonylation of methanol to acetic acid over Rh/Ys catalyst

A novel catalyst Rh/Ys for the carbonylation of methanol to acetic acid with CH3I as the promoter shows excellent activity and selectivity.The reaction is kinetically controlled.The reaction rate is in proportion to the concentration of Rh and CH3I but has nothing to do with those of CH3OHH and CO.The surface active energy is Ea ~51.02 kJ/mol.A mechanism is also proposed.     

Catalytic double carbonylation of epoxides to succinic anhydrides: catalyst discovery, reaction scope, and mechanism

The first catalytic method for the efficient conversion of epoxides to succinic anhydrides via one-pot double carbonylation is reported. This reaction occurs in two stages: first, the epoxide is carbonylated to a beta-lactone, and then the beta-lactone is subsequently carbonylated to a succinic anhydride. This reaction is made possible by the bimetallic catalyst [(ClTPP)Al(THF)2]+[Co(CO)4]- (1; ClTPP = meso-tetra(4-chlorophenyl)porphyrinato; THF = tetrahydrofuran), which is highly active and selective for both epoxide and lactone carbonylation, and by the identification of a solvent that facilitates both stages. The catalysis is compatible with substituted epoxides having aliphatic, aromatic, alkene, ether, ester, alcohol, nitrile, and amide functional groups. Disubstituted and enantiomerically pure anhydrides are synthesized from epoxides with excellent retention of stereochemical purity. The mechanism of epoxide double carbonylation with 1 was investigated by in situ IR spectroscopy, which reveals that the two carbonylation stages are sequential and non-overlapping, such that epoxide carbonylation goes to completion before any of the intermediate beta-lactone is consumed. The rates of both epoxide and lactone carbonylation are independent of carbon monoxide pressure and are first-order in the concentration of 1. The stages differ in that the rate of epoxide carbonylation is independent of substrate concentration and first-order in donor solvent, whereas the rate of lactone carbonylation is first-order in lactone and inversely dependent on the concentration of donor solvent. The opposite solvent effects and substrate order for these two stages are rationalized in terms of different resting states and rate-determining steps for each carbonylation reaction.